Abstract: A processing system receives a user-generated media recording, and metadata associated with the user-generated feedback, from a first device. The user-generated media recording is a recording of the public end-user captured during a live media broadcast using a public-user interface on the first device. The metadata includes information linking the user-generated media recording to the live media broadcast. The system stores the user-generated media recording and the first metadata in one or more storage devices, and transmits a version of the user-generated media recording and at least a portion of the first metadata to a private-user interface on a second device. The private-user interface is configured to receive input from a private end-user selecting the version of the user-generated media recording for broadcast during the same live media broadcast during which the user-generated media recording was created.

Abstract: A creeper for scooting around on top of decking for decking installation, maintenance, and/or repair activities may minimize injury to a human user's knees and/or back. Movement-means of the creeper, such as, but not limited to, casters may be attached at or near a bottom of a base of the creeper to facilitate such scooting around. A seat may be attached to a top of the base of the creeper, wherein the seat may be sat upon by the human user during use of the creeper. Also attached to the base of the creeper may be a drill-guide. The drill-guide may facilitate controlled and repeatable predrilling of pilot holes, at predetermined angles (e.g., perpendicular) into decking planks and/or into joists. The creeper may also facilitate attachment of decking members, with the pilot holes, to joists.

Abstract: The present invention provides a process for the preparation of ethene by vapour phase chemical dehydration of ethanol using an adiabatic reactor, wherein the interior of the adiabatic reactor is separated into at least three reaction zones, comprising a first reaction zone, at least one intermediate reaction zone and a final reaction zone, and wherein each zone contains an ethanol dehydration catalyst; said process comprising the steps of; a) feeding a pre-heated reactant feed-stream into an inlet of the first reaction zone; b) extracting an effluent-stream from an outlet of the first reaction zone; c) feeding said effluent-stream into an inlet of a subsequent intermediate reaction zone; d) extracting an effluent-stream from an outlet of the intermediate reaction zone; e) repeating steps (c) and (d) for any subsequent intermediate reaction zones, if present; f) feeding, into an inlet of the final reaction zone, the effluent-stream from the preceding intermediate reaction zone; g) extracting a product stream

Abstract: Ergonomic protective cone collars for pets, their use, and positioning are disclosed. Such cone-collars may be made of two main sections, a cone-like-structure and an integral-collar that may be attached to a base of the cone-like-structure. The integral-collar may be collar like, intended to be worn and fastened around a neck of the animal. The cone-like-structure may be made from a plurality of radially-oriented-tapered-pockets, that due to their fill and/or material of construction may be semi-rigid, imparting a degree of inherent stiffness, flexibility, and/or elasticity. The plurality of radially-oriented-tapered-pockets may be of different lengths such that the cone-like-structure has an overall scalloped shape which may provide for several benefits, such as proper coverage proximate to the animal's mouth region and less visually obscuring material at the sides of the animal's head. A cone-collar may be positioned properly on the animal via removable attachment to a harness worn by the animal.

Abstract: Ergonomic protective cone collars for pets, their use, and positioning are disclosed. Such cone-collars may be made of two main sections, a cone-like-structure and an integral-collar that may be attached to a base of the cone-like-structure. The integral-collar may be collar like, intended to be worn and fastened around a neck of the animal. The cone-like-structure may be made from a plurality of radially-oriented-tapered-pockets, that due to their fill and/or material of construction may be semi-rigid, imparting a degree of inherent stiffness, flexibility, and/or elasticity. The plurality of radially-oriented-tapered-pockets may be of different lengths such that the cone-like-structure has an overall scalloped shape which may provide for several benefits, such as proper coverage proximate to the animal's mouth region and less visually obscuring material at the sides of the animal's head. A cone-collar may be positioned properly on the animal via removable attachment to a harness worn by the animal.

Abstract: Process for the production of ethanol from acetic acid and hydrogen, said process comprising: reacting in an esterification reaction vessel methanol with acetic acid in the presence of an esterification catalyst and an entrainer to form a product comprising entrainer, methyl acetate and water, and in a distillation column, recovering from the product an overhead product fraction comprising methyl acetate, methanol and water, feeding the overhead product fraction, together with hydrogen, into a hydrogenation unit containing a copper based hydrogenation catalyst, to produce a hydrogenation product stream comprising ethanol, methanol, unreacted methyl acetate, unreacted hydrogen, ethyl acetate and water, cooling the hydrogenation product stream; separating the cooled hydrogenation product stream into a liquid phase which comprises the majority of the methanol, ethanol, methyl acetate, ethyl acetate and water, and a gaseous phase which comprises the majority of the unreacted hydrogen; recycling at least part of t

Abstract: Hydrogenation of methyl acetate to methanol and ethanol by feeding a hydrogenation feed of methyl acetate, water, hydrogen and a carbon oxide into a hydrogenation unit containing a copper-zinc oxide hydrogenation catalyst to produce a hydrogenation product stream of ethanol, methanol, unreacted methyl acetate, water, unreacted hydrogen, carbon monoxide, carbon dioxide, and ethyl acetate. The hydrogenation unit is operated in the vapor phase at elevated temperature and pressure. The total molar ratio of hydrogen to methyl acetate fed to the hydrogenation unit is 5:1 to 20:1. The total molar ratio of methyl acetate to carbon oxide(s) fed to the hydrogenation unit is 1:2 to 100:1. The hydrogenation product stream is separated into a liquid stream containing ethanol, methanol, unreacted methyl acetate, water and ethyl acetate, and a gaseous stream containing unreacted hydrogen, carbon monoxide and carbon dioxide, and a portion of the gaseous stream is recycled to the hydrogenation unit.

Abstract: Provided are methods for removing one or more components from a butanol based composition. The methods comprise providing a butanol based composition comprising one or more components, targeting at least one component or a combination thereof for reduction, and processing said butanol based composition such that the at least one targeted component is substantially removed. The butanol based composition can, for example, be bio-produced.

Abstract: The present invention provides a process for the preparation of ethene by vapour phase chemical dehydration of ethanol using an adiabatic reactor, wherein the interior of the adiabatic reactor is separated into at least three reaction zones, comprising a first reaction zone, at least one intermediate reaction zone and a final reaction zone, and wherein each zone contains an ethanol dehydration catalyst; said process comprising the steps of; a) feeding a pre-heated reactant feed-stream into an inlet of the first reaction zone; b) extracting an effluent-stream from an outlet of the first reaction zone; c) feeding said effluent-stream into an inlet of a subsequent intermediate reaction zone; d) extracting an effluent-stream from an outlet of the intermediate reaction zone; e) repeating steps (c) and (d) for any subsequent intermediate reaction zones, if present; f) feeding, into an inlet of the final reaction zone, the effluent-stream from the preceding intermediate reaction zone; g) extracting a product stream

Abstract: A process for the acid-catalyzed dehydration of ethanol, the process comprising the steps of distilling an ethanol feedstock (101) comprising at least one nitrogen-containing contaminant to form an overhead stream (102) and a bottom stream comprising ethanol (103), wherein the distillation has a reflux ratio of at least 20:1; and reacting the bottom stream in the presence of an acid catalyst to form a product stream comprising ethylene.

Abstract: Provided are methods for removing one or more components from a butanol based composition. The methods comprise providing a butanol based composition comprising one or more components, targeting at least one component or a combination thereof for reduction, and processing said butanol based composition such that the at least one targeted component is substantially removed. The butanol based composition can, for example, be bio-produced.

Abstract: Process for reducing the water and carboxylic acid content of an alcohol composition containing at least one alcohol having one to four carbon atoms, water and at least one carboxylic acid having from one to four carbon atoms by contacting the alcohol composition with a desiccant bed containing at least one porous inorganic oxide material at elevated temperature. At least one of the porous inorganic oxide material(s) contains Brønsted acid sites and/or neutralized Brønsted acid sites.

Abstract: A process for the hydrogenation of methyl acetate to methanol and ethanol comprising feeding a hydrogenation feed composition comprising methyl acetate and water, together with hydrogen and at least one carbon oxide selected from carbon monoxide and carbon dioxide, into a hydrogenation unit containing a copper-zinc oxide hydrogenation catalyst and hydrogenating the methyl acetate to produce a hydrogenation product stream comprising ethanol, methanol, unreacted methyl acetate, water, unreacted hydrogen, carbon monoxide, carbon dioxide, and ethyl acetate, wherein said hydrogenation unit is operated in the vapour phase at elevated temperature, preferably at a temperature in the range of from 180 to 270° C.

Abstract: The invention relates to a method for producing butanol through microbial fermentation, in which the butanol product is removed by extraction into a water immiscible organic extractant during the fermentation. The invention also relates to a method for producing butanol through microbial fermentation, in which the butanol product is removed during the fermentation by extraction into a water-immiscible extractant composition. The invention further relates to compositions comprising a solution of butanol in a water immiscible organic extractant composition.

Abstract: The invention relates to a method for producing butanol through microbial fermentation, in which the butanol product is removed by extraction into a water immiscible organic extractant during the fermentation. The invention also relates to a method for producing butanol through microbial fermentation, in which the butanol product is removed during the fermentation by extraction into a water-immiscible extractant composition. The invention further relates to compositions comprising a solution of butanol in a water immiscible organic extractant composition.

Abstract: Process for the production of ethanol from acetic acid and hydrogen, said process comprising: reacting in an esterification reaction vessel methanol with acetic acid in the presence of an esterification catalyst and an entrainer to form a product comprising entrainer, methyl acetate and water, and in a distillation column, recovering from the product an overhead product fraction comprising methyl acetate, methanol and water, feeding the overhead product fraction, together with hydrogen, into a hydrogenation unit containing a copper based hydrogenation catalyst, to produce a hydrogenation product stream comprising ethanol, methanol, unreacted methyl acetate, unreacted hydrogen, ethyl acetate and water, cooling the hydrogenation product stream; separating the cooled hydrogenation product stream into a liquid phase which comprises the majority of the methanol, ethanol, methyl acetate, ethyl acetate and water, and a gaseous phase which comprises the majority of the unreacted hydrogen; recycling at least part of t